where g1 and g2
are the liquid phase activity coefficients for species 1 and 2 and where A12, A21
and C are the parameters.
The program has the following characteristics:
- Data are assumed to be in the form of pressure P vs. liquid phase mole fraction x1
for a binary system at constant temperature.
- The vapor phase is assumed to be an ideal gas and Poynting corrections are assumed
to be negligible.
- The program determines the optimum 4-suffix parameters A12, A21
and C by minimizing the sum of the squares of the differences between the experimental and
calculated pressures. The flexible polyhedron search of Nelder and Mead is used.
- Output consists of the optimum 4-suffix Margules parameters and resulting calculated
pressures and vapor phase compositions y1 for each experimental x1
value. Values of deviations between experimental and calculated pressures also are
given.
Click here to regress an example set of data
(Acetone(1)+Toluene(2) at 30 oC).
Click here to enter your own set of vapor liquid
equilibrium data.
Click here to return Home.